JPH03293091A - Waste water electrolyzing device - Google Patents
Waste water electrolyzing deviceInfo
- Publication number
- JPH03293091A JPH03293091A JP9417790A JP9417790A JPH03293091A JP H03293091 A JPH03293091 A JP H03293091A JP 9417790 A JP9417790 A JP 9417790A JP 9417790 A JP9417790 A JP 9417790A JP H03293091 A JPH03293091 A JP H03293091A
- Authority
- JP
- Japan
- Prior art keywords
- plates
- wastewater
- electrolytic treatment
- electrode plates
- electrolytic
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000002351 wastewater Substances 0.000 title claims abstract description 39
- 238000007790 scraping Methods 0.000 claims abstract description 26
- 239000012212 insulator Substances 0.000 claims abstract description 3
- 210000005056 cell body Anatomy 0.000 claims description 6
- 230000002093 peripheral effect Effects 0.000 claims description 4
- 239000011347 resin Substances 0.000 claims description 4
- 229920005989 resin Polymers 0.000 claims description 4
- 239000003792 electrolyte Substances 0.000 claims 2
- 239000002244 precipitate Substances 0.000 abstract description 13
- 230000008021 deposition Effects 0.000 abstract 1
- 210000004027 cell Anatomy 0.000 description 16
- 238000004891 communication Methods 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 238000005554 pickling Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 239000004809 Teflon Substances 0.000 description 3
- 229920006362 Teflon® Polymers 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- -1 polytetrafluoroethylene Polymers 0.000 description 3
- 238000004065 wastewater treatment Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- 229910000640 Fe alloy Inorganic materials 0.000 description 1
- 240000002853 Nelumbo nucifera Species 0.000 description 1
- 235000006508 Nelumbo nucifera Nutrition 0.000 description 1
- 235000006510 Nelumbo pentapetala Nutrition 0.000 description 1
- 229920002292 Nylon 6 Polymers 0.000 description 1
- 229920002302 Nylon 6,6 Polymers 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- XECAHXYUAAWDEL-UHFFFAOYSA-N acrylonitrile butadiene styrene Chemical compound C=CC=C.C=CC#N.C=CC1=CC=CC=C1 XECAHXYUAAWDEL-UHFFFAOYSA-N 0.000 description 1
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 1
- 239000004676 acrylonitrile butadiene styrene Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000007822 coupling agent Substances 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000003657 drainage water Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 231100001231 less toxic Toxicity 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 235000021110 pickles Nutrition 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 239000004810 polytetrafluoroethylene Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000003440 toxic substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野]
本発明は、排水の電解処理装置に関し、特に継続稼働す
ることができる電解処理装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an electrolytic treatment device for wastewater, and particularly to an electrolytic treatment device that can be operated continuously.
公害防止の見地から、多くの極性分子やイオンの形態を
した水溶性化合物を溶解した工業排水を、電解方式によ
り一定排出基準値まで浄化することが求められる。従来
のこの種の技術としては、1)米国特許第3.926,
754号、2)同第4.036,726号、3)同第4
,123.339号及び4)ヨーロッパ特許出願公開第
285,696号各明細書などに、その原理や、各種の
方法や装置、効果が開示されている。From the standpoint of pollution prevention, it is necessary to purify industrial wastewater containing dissolved water-soluble compounds in the form of many polar molecules and ions to a certain emission standard value using an electrolytic method. Conventional technologies of this type include: 1) U.S. Patent No. 3.926;
No. 754, 2) No. 4.036,726, 3) No. 4
, 123.339 and 4) European Patent Application Publication No. 285,696, the principles, various methods, devices, and effects thereof are disclosed.
これらはおおよそ、電解槽内の一定間隔に交互に平行配
置された陰陽両極板間に排水を流し、極板に電流を通す
ことにより前記排水を電解し、水溶性化合物などを不溶
性沈殿物に化して除去するか、または、成分によっては
化学反応により有害物質を無害又は毒性の低い物質に変
えるように構成される。そのうち、前記1)では極板を
垂直面に沿って平行配置した装置構成が開示されている
。These methods generally involve flowing wastewater between negative and positive electrode plates arranged in parallel at regular intervals in an electrolytic cell, electrolyzing the wastewater by passing an electric current through the plates, and turning water-soluble compounds into insoluble precipitates. Depending on the component, it is designed to remove harmful substances or, depending on the ingredients, to convert harmful substances into harmless or less toxic substances through chemical reactions. Among them, 1) discloses a device configuration in which the electrode plates are arranged in parallel along a vertical plane.
しかし、前記3)の記載によれば、実用化規格の処理シ
ステムにおいては生成沈殿物が極板の材質によっては極
板に沈積し、または液の通路に堆積し、次第に塊が大き
くなれば液流を妨げるのみでなく、極板に沈殿物が付着
するため電圧が上昇し、また表面に酸素の気泡が発生す
るため、これらの問題を解決するのに、定期的に槽内を
希釈無機酸液により回流洗浄して極板の付着物を除去し
なくてはならないとある。このように定期的な極板の酸
洗処理は、電解処理作業を止めて施さなくてはならず、
また電解処理と酸洗処理とが一貫連続実施できるように
するべく、排水の電解処理システムの配管路に、前記3
)が示す如く酸洗処理システムの配管路をバイパスさせ
る必要があると共に、電解処理作業の他に定期的に、電
解槽内の排水放出工程、酸洗処理工程及び酸洗液の回収
工程を要するなどの面倒も伴ってくる。However, according to the description in 3) above, in a treatment system that meets practical standards, depending on the material of the electrode plate, the generated precipitate is deposited on the electrode plate or deposited in the liquid passage, and if the lumps gradually become larger, the In addition to impeding the flow, the voltage increases due to the accumulation of precipitates on the electrode plates, and oxygen bubbles are generated on the surface.To solve these problems, periodically dilute the tank with inorganic acid. It says that the deposits on the electrode plates must be removed by circulating cleaning with liquid. In this way, periodic pickling of the electrode plates must be carried out after stopping the electrolytic treatment.
In addition, in order to be able to carry out electrolytic treatment and pickling treatment consistently and continuously, the above-mentioned three
), it is necessary to bypass the piping of the pickling treatment system, and in addition to the electrolytic treatment work, it is necessary to periodically discharge the waste water in the electrolytic cell, pickle treatment process, and collect the pickling liquid. It also comes with other troubles.
本発明は、これらに鑑みてなされたもので、排水の電解
処理作業を中断させることなく、常に継続稼働すること
ができる排水の電解処理装置を提供しようとするもので
ある。The present invention has been made in view of these circumstances, and it is an object of the present invention to provide a wastewater electrolytic treatment apparatus that can be continuously operated without interrupting the wastewater electrolytic treatment work.
本発明はまた、前記排水の電解処理装置において、排水
がよどみな(かつ十分に電解極板と接触することができ
る電解処理装置を提供しようとするものである。Another object of the present invention is to provide an electrolytic treatment apparatus for wastewater in which the wastewater does not stagnate (and can sufficiently come into contact with the electrolytic electrode plate).
本発明はまた、前記排水の電解処理装置において、排水
処理容量を弾力的に増減可能な電解処理装置を提供しよ
うとするものである。The present invention also provides an electrolytic treatment device for wastewater that can flexibly increase or decrease its wastewater treatment capacity.
したがって、本発明の装置は、電解槽本体の内部に一定
間隔をおいて平板状の互いに絶縁状態の陰陽両極性の電
解極板を平行に配置し、排水を前記両極板間に回流させ
ると同時に、両極板に電流を通すようにしてなる排水の
電解処理装置において、隣接して対向する前記陰陽両極
板の間に、これらの対向両極板の表面に両側縁エツジ部
を当接して駆動手段によって移動されて、それにより前
記両極板の表面を摺動する絶縁体掻取部材を設けてなる
ように構成される。Therefore, in the device of the present invention, flat plate-shaped electrolytic electrode plates of negative and positive polarity, which are insulated from each other, are arranged in parallel at regular intervals inside an electrolytic cell body, and waste water is circulated between the two electrode plates, and at the same time , in a wastewater electrolytic treatment apparatus configured to pass current through bipolar plates, the electrode is moved by a driving means between the negative and anode bipolar plates which are adjacent to each other and are brought into contact with the surfaces of these opposing bipolar plates. Accordingly, an insulator scraping member that slides on the surface of the bipolar plate is provided.
本発明はまた前記装置において、前記掻取部材は、テフ
ロン(ポリテトラフルオロエチレンの商品名)など弾性
変形可能な樹脂により当接摺動する両側縁がエツジ部を
なすように形成され、そして前記駆動手段は、各極板の
ほぼ中心部を貫通するように軸架されてモータにより駆
動される回転軸と、回転軸の各極板間の位置からほぼ回
転半径方向へ突設された前δ己掻取部材を保持する腕部
材とにより構成される。The present invention also provides the above device, wherein the scraping member is formed of an elastically deformable resin such as Teflon (trade name of polytetrafluoroethylene) so that both side edges that come into contact and slide form edge portions; The driving means includes a rotating shaft that is mounted so as to pass through approximately the center of each electrode plate and is driven by a motor, and a front δ that protrudes approximately in the direction of the rotation radius from a position between each electrode plate of the rotating shaft. and an arm member that holds the self-scraping member.
本発明の前記装置は、前記構成に加えて、各極板を、そ
れらがほぼ水平面に沿って下から上へ平行配置され、そ
れぞれの外周縁部が電解槽の内壁と水密に連接されると
共に、各極板には排水を流通させるための流通孔を貫設
して、各極板がこれらの流通孔が隣接極板どうしでは互
いにそれらの極板の相対する側に位置するように配置さ
れるように構成する。In addition to the above-described configuration, the device of the present invention has the respective electrode plates arranged in parallel from bottom to top along a substantially horizontal plane, each outer peripheral edge being watertightly connected to the inner wall of the electrolytic cell. Each electrode plate is provided with a through hole for distributing wastewater, and each electrode plate is arranged such that these flow holes are located on opposite sides of adjacent electrode plates. Configure it so that
なお、各極板がほぼ水平面に沿って下から上へ平行配置
される前記装置において、電解槽は、各極板ごとに1個
ずつの独自に1枚の極板を水密保持可能なフープ状節部
材を相互に水密に連接させて構成される。In addition, in the above-mentioned device in which each electrode plate is arranged in parallel from bottom to top along a substantially horizontal plane, the electrolytic cell is formed into a hoop-shaped cell that can independently hold one electrode plate watertight for each electrode plate. It is constructed by connecting joint members in a watertight manner.
前記のほかに、本発明における電解槽の横断面形状は円
形や楕円形、正方形、多角形のいかんを問わないが、掻
取部材の運動形態から見て円形が好ましく、少なくとも
内周面は円形であることが好ましい。In addition to the above, the cross-sectional shape of the electrolytic cell in the present invention may be circular, oval, square, or polygonal, but it is preferably circular in view of the movement form of the scraping member, and at least the inner peripheral surface is circular. It is preferable that
また、前記電解極板の材質は、処理排水の特性や化学成
分に応じて鉄や、鋼鉄、ステンレス鋼、他の鉄合金、ア
ルミ、アルミ合金などから選ぶことができる。The material of the electrolytic electrode plate can be selected from iron, steel, stainless steel, other iron alloys, aluminum, aluminum alloys, etc. depending on the characteristics and chemical composition of the treated wastewater.
前記掻取部材の材質は絶縁性が必須であり、出来れば化
学的に耐強酸、強アルカリ性や耐腐蝕性をそなえ、十分
な機械的強さがあって高温下でもこれらの性質が安定な
ものが望ましく、たとえば、PVCやポリプロピレン、
ポリエチレン、ポリテトラフルオロエチレン(テフロン
)、アクリロニトリルブタジェンスチレン共重合体、ナ
イロン6、ナイロン66、などの樹脂類を単独に、また
はこれらのいずれかをガラス繊維或いはカーボン繊維に
より強化した複合材などを使用することができる。本発
明の一実施例においては、テフロン製掻取部材を用いた
が、エツジ部に電極板面に対し適当な粗さをもたせて掻
取効果を高めることを図って、テフロンに適量のガラス
ピーズを添加すると同時に、カップリング剤により両者
の付着力を強化している。The material of the scraping member must be insulating, preferably chemically resistant to strong acids, strong alkalis, and corrosion, and has sufficient mechanical strength and these properties are stable even at high temperatures. For example, PVC, polypropylene,
Polyethylene, polytetrafluoroethylene (Teflon), acrylonitrile butadiene styrene copolymer, nylon 6, nylon 66, and other resins alone, or composite materials made by reinforcing any of these with glass fiber or carbon fiber. can be used. In one embodiment of the present invention, a Teflon scraping member was used, but in order to increase the scraping effect by giving the edge part an appropriate roughness to the electrode plate surface, an appropriate amount of glass beads was added to the Teflon. At the same time, a coupling agent is used to strengthen the adhesion between the two.
[作 用]
本発明の前記排水の電解処理装置の構成によれば、電解
槽内部の極板の間に掻取部材を両極板表面と摺接させて
設け、かつ両極板表面に対して掻取部材を移動するよう
に駆動手段を設けたことにより、排水の電解処理中、掻
取部材を極板表面に対して常に摺動させて、極板表面に
生成または付着した物質が常時掻き取られるようになる
。[Function] According to the configuration of the electrolytic treatment apparatus for wastewater of the present invention, a scraping member is provided between the electrode plates inside the electrolytic cell in sliding contact with the surfaces of the two electrode plates, and the scraping member is provided on the surfaces of the two electrode plates. By providing a driving means to move the electrode, the scraping member is constantly slid against the electrode plate surface during the electrolytic treatment of wastewater, so that substances generated or attached to the electrode plate surface are constantly scraped off. become.
前記装置において、本発明のごとく、極板を横にして下
から上へ積層状に配置し、各隣接極板にそれぞれ逆側縁
部に交互に液の流通孔を穿設して曲折した流路を形成す
ることにより、排水が十分極板と接触するようになる。In the above device, as in the present invention, the electrode plates are arranged horizontally in a stacked manner from bottom to top, and liquid flow holes are alternately bored in the opposite edges of each adjacent electrode plate to form a curved flow. By forming the channel, sufficient drainage water is brought into contact with the plate.
本発明の前記装置において、電解槽を各電解極板ごとに
1個ずつ対応するフープ状の節部材からて構成される電
解槽容量、すなわち、排水処理能力の加減をすることが
できる。In the apparatus of the present invention, the capacity of the electrolytic cell, that is, the wastewater treatment capacity, can be adjusted by forming the electrolytic cell from hoop-shaped joint members, one for each electrolytic plate.
以下、本発明の実施例を図面にもとすき説明す先端を底
部材60に軸支された角形断面の回転軸70に各極板の
位置から外向きに突設された腕部材30に取り付けられ
、モータ90の回転駆動によって移動されることにより
その両側縁エツジ部を対向する両極板20の表面に当て
て摺動される掻取部材40とから主として構成される。Hereinafter, embodiments of the present invention will be described with reference to the drawings.The tip is attached to an arm member 30 that protrudes outward from the position of each electrode plate on a rotating shaft 70 with a square cross section that is pivotally supported on a bottom member 60. The scraping member 40 is moved by the rotational drive of the motor 90 and is slid by applying the edge portions of both side edges thereof to the surfaces of the opposing bipolar plates 20.
以下、前記各構成のうち、要部の詳細を第12図と共に
第3図(a)、 (b)、 (C)を参照して説明する
。Hereinafter, details of the main parts of each of the above configurations will be explained with reference to FIG. 12 as well as FIGS. 3(a), (b), and (C).
各節部材IOは、A B−3樹脂から成形され、そ排水
電解処理装置100は、処理しようとする排水量により
決まる節数の節部材10を上下方向へ積層状に組み合わ
せ、上蓋部材50及び底蓋部材60と共にタイロッド1
9により集成されてなる電解槽の槽本体1と、この槽本
体lの内部に、それぞれ各節部材IOに1枚ずつ保持さ
れその端子21を交互に陰陽逆性の電源接続ハス80に
接続された電解極板20と、槽本体1を軸心線に沿って
上蓋部材50から各極板20を串刺しに突き抜けてそれ
ぞれに設けられた輪溝11L112に各シールリング1
4を収容し、外周縁部分には等間隔の8箇所にそれぞれ
通孔16が穿設されたラグが形成され、かつ1か所に円
座13を外部と連通させる欠は口15が設けられる(第
3図(a))。Each node member IO is molded from A B-3 resin, and the wastewater electrolytic treatment apparatus 100 combines the node members 10, the number of which is determined by the amount of wastewater to be treated, in a stacked manner in the vertical direction, and includes a top cover member 50 and a bottom. Tie rod 1 together with lid member 60
A cell body 1 of an electrolytic cell is assembled with 9, and inside this cell body 1, one plate is held in each joint member IO, and its terminals 21 are alternately connected to a power connection lotus 80 of negative and negative polarity. Each seal ring 1 is inserted into an annular groove 11L112 provided in each electrode plate 20 by skewering each electrode plate 20 from the upper cover member 50 along the axis of the tank body 1.
A lug is formed on the outer periphery with through holes 16 formed at eight equally spaced locations, and a hole 15 is provided at one location to communicate the conical seat 13 with the outside. (Figure 3(a)).
各電解極板20は、この例では鉄鋼板材からほぼ前記円
座12に嵌合する外径の円板形に成形され、円周の1か
所に前記欠は口15から伸出することができる接続端子
部21が突設され、この端子部21の中央に接続用のね
し孔211が穿設され、ほぼ端子部21の位置から90
度面回転た円周部に弓形の流通孔23と、また円心部に
前記回転輪70を遊挿させる軸孔22とが開設される。In this example, each electrolytic electrode plate 20 is formed from a steel plate material into a disc shape with an outer diameter that fits approximately into the circular seat 12, and has a notch at one location on the circumference that extends from the opening 15. A connecting terminal portion 21 is provided in a protruding manner, and a threaded hole 211 for connection is bored in the center of this terminal portion 21, approximately 90 degrees from the position of the terminal portion 21.
An arcuate communication hole 23 is provided in the circumferential portion of the rotor, and an axial hole 22 is provided in the center portion of the circle, into which the rotary ring 70 is loosely inserted.
前記極板20の互いの隙間に半径方向へ沿って介在する
腕部材30は、一端の角孔31で回転軸70と連動可能
に係合し、他方の回転端部32は長手方向の割り溝33
によりホーク状に形成されている。The arm member 30 interposed in the gap between the electrode plates 20 along the radial direction is operatively engaged with the rotating shaft 70 through a square hole 31 at one end, and the other rotating end 32 is provided with a slot in the longitudinal direction. 33
It is formed into a hawk shape.
掻取部材40は、第4図に示されるように、やや末広に
開口する細長の溝型バー状を呈し、溝の底部41を前記
割り溝33に挟ませることにより横方向に開口して腕部
材30の回転端部32に保持され、両側壁部42の先端
縁に拡張方向へエツジ部43が設けられ、上下両極板2
0の表面に弾力当接するようされる。As shown in FIG. 4, the scraping member 40 has an elongated groove-shaped bar shape with a slightly wider opening, and the bottom part 41 of the groove is sandwiched between the split grooves 33 to open laterally and form an arm. It is held by the rotating end portion 32 of the member 30, and edge portions 43 are provided at the distal edges of both side wall portions 42 in the expansion direction, and the upper and lower bipolar plates 2
It is made to come into elastic contact with the surface of 0.
上蓋部材50は、中心部に軸孔51が、それの近くに流
出口52が、また周縁部に8個の前記節部材100通孔
16と対応する通孔53がそれぞれ設けられた円盤状に
なっている。The upper cover member 50 has a disc shape with a shaft hole 51 in the center, an outlet 52 near the shaft hole, and a through hole 53 corresponding to the eight through holes 16 of the node member 100 in the peripheral portion. It has become.
底蓋部材60は、ほぼ前記上蓋部材50と上下対応する
円盤状をし、中心部に対面側へ突き出すように凹陥した
軸受シー)61が、その近くに流入口62が、かつ周縁
部の8か所の等間隔位置に通孔63がそれぞれ設けられ
、底面部には、流入口62の開口に管継手64と、移動
可能にさせる支持フレーム65が取り付けられている。The bottom cover member 60 has a disc shape that corresponds vertically to the top cover member 50, and has a bearing seat 61 in the center that is recessed so as to protrude toward the opposite side, an inlet port 62 near the bearing seat 61, and an inlet 8 on the periphery. Through holes 63 are provided at equally spaced positions, and a pipe joint 64 and a movable support frame 65 are attached to the bottom surface of the inlet 62 .
本実施例における駆動手段は、前記腕部材30と、これ
が取り付けられた回転軸70と、これらを回転駆動する
モータ90とで構成される。回転軸70は、角形の軸杆
部71を前記槽本体1内に突込み、下端を軸受け72を
介して軸受シート61に軸着され、各極板20.20間
位置に前位置部材30を係合させ、上端シャンク部73
を、詳細は略すが、上蓋部材50の軸孔51から外部へ
伸出したのち、継手74により上方部に支架されたモー
タ90の出力軸91と連結され、伝動回転される。なお
、軸杆71の極板20を挿通ずる部分には、その角孔に
より外嵌する環状ブツシュ25と、極板20の軸孔22
に嵌合されるリングメタル24とが滑り自在に介在して
いる(第3図(C))。The driving means in this embodiment includes the arm member 30, a rotating shaft 70 to which the arm member 30 is attached, and a motor 90 that rotationally drives these members. The rotating shaft 70 has a rectangular shaft rod part 71 inserted into the tank body 1, and its lower end is pivotally attached to the bearing seat 61 via a bearing 72, and the front position member 30 is engaged between the pole plates 20 and 20. the upper end shank part 73
Although the details are omitted, after extending to the outside from the shaft hole 51 of the upper cover member 50, it is connected to the output shaft 91 of the motor 90 supported at the upper part by a joint 74, and is driven and rotated. In addition, in the part of the shaft rod 71 through which the pole plate 20 is inserted, there is an annular bushing 25 which is externally fitted through the square hole thereof, and a shaft hole 22 of the pole plate 20.
A ring metal 24, which is fitted into the ring metal 24, is slidably interposed therebetween (FIG. 3(C)).
本実施例の前記構成による装置100は、所定数の各電
解極板20を節部材IOの内径の小さな円座12にシー
ルリング14を介して嵌合し、端子部21を欠は口15
から伸出させた状態で底蓋部材60上に積層状に積み上
げ(第3図(b))、その次に上蓋部材50を最上節に
置き、この際、各極板20を、1iff置きの端子部2
1が隣接節の端子部21と互いに180度相対し、それ
ぞれ陰陽極に分かれて2列になるように配列すると同時
に、これとはほぼ90度離れて1節置きの流通孔23が
互いに相対する側に並ぶように節部材10を回して調整
することにより配置する。そして、回転軸70は底蓋部
材60に先端を軸着すると共に、各極板20間にそれぞ
れ前記のごとく掻取部材40を装着した腕部材30を係
合させた状態でモータ90へ連動連結させる。かくて、
前記状態の各極板20のそれぞれ互いに対応する通孔1
6と、上蓋部材50の通孔53と、底蓋部材60の通孔
63とが、上下方向に一直線に並ぶので、各列それぞれ
をタイロッド19で挿通してねじ締め手段などにより締
め合わせ、水密な電解槽1にする。続いて、前記上下に
2列に並んだ端子部21を、各々同一のバス80にねじ
付は連接し、その一方のバス80は電源の陰極と、他方
のハス80は陽極とそれぞれ接続させる。In the device 100 according to the above configuration of the present embodiment, a predetermined number of electrolytic electrode plates 20 are fitted into a circular seat 12 having a small inner diameter of a joint member IO via a seal ring 14, and a terminal portion 21 is inserted into a hole 15.
The top cover member 50 is placed in a stacked manner on the bottom cover member 60 in the extended state (FIG. 3(b)), and then the top cover member 50 is placed on the top node. At this time, each electrode plate 20 is Terminal part 2
1 and the terminal portions 21 of adjacent nodes are arranged at 180 degrees to each other, each divided into cathodes and anodes and arranged in two rows, and at the same time, the communication holes 23 at every other node are separated from this by approximately 90 degrees and are opposed to each other. They are arranged by turning and adjusting the joint members 10 so that they are lined up side by side. The rotating shaft 70 has its tip pivotally attached to the bottom cover member 60, and is operatively connected to the motor 90 with the arm member 30 having the scraping member 40 attached thereto as described above engaged between each electrode plate 20. let Thus,
Through holes 1 corresponding to each other in each electrode plate 20 in the above state
6, the through hole 53 of the top cover member 50, and the through hole 63 of the bottom cover member 60 are lined up in a straight line in the vertical direction, so each row is inserted with a tie rod 19 and tightened using screw tightening means or the like to make it watertight. Make electrolytic cell 1. Subsequently, the terminal portions 21 arranged in two vertical rows are connected to the same bus 80 with screws, and one bus 80 is connected to the cathode of the power source, and the other bus 80 is connected to the anode.
前記装置100は、排水を管路より管継手64をへて流
入口62から送り込み、前記バス80より全極板20に
電圧を印加すれば、排水は電解槽l内を、第6図の略示
線図に矢印で示すように、各極板20間とそれぞれの流
通孔23により形成されるジグザグ通路を回流し、その
間に電解処理されて前記流出口52より排出されるよう
になる。In the device 100, if waste water is sent from the pipe through the pipe joint 64 and from the inlet 62, and a voltage is applied to all the electrode plates 20 from the bus 80, the waste water flows inside the electrolytic cell l as shown in FIG. As shown by the arrows in the diagram, the liquid flows through the zigzag passages formed between the electrode plates 20 and the respective communication holes 23, and is electrolytically treated during this period and discharged from the outlet 52.
そして、電解により析出して極板20に沈積または付着
した析出沈殿物は、モータ90の駆動により回転伝動さ
れて回転軸70の腕部材30が回転するので、第5図に
図すように、これに取り付けられた掻取部材40も回転
し、これに伴いエツジ部43が極板20の表面に摺接移
動し、前記析出沈殿物を掻取るようになり、電解処理中
モータ90を連続回転させれば、この掻取操作が継続さ
れる。The precipitates deposited or attached to the electrode plate 20 by electrolysis are rotated by the drive of the motor 90, and the arm member 30 of the rotating shaft 70 rotates, so that as shown in FIG. The scraping member 40 attached to this also rotates, and the edge portion 43 moves in sliding contact with the surface of the electrode plate 20 to scrape off the precipitate, causing the motor 90 to continuously rotate during the electrolytic treatment. If you do so, this scraping operation will continue.
なお、掻取られた沈殿物は、排水と共に流出口52より
排出され、沈殿除去処理されるのであるが、公知なので
説明は省く。Note that the scraped precipitate is discharged from the outlet 52 together with the waste water and subjected to a precipitate removal treatment, but since this is well known, the explanation will be omitted.
本発明によれば、電解により析出して極板20に沈積ま
たは付着した析出沈殿物は、モータ90の駆動により回
転伝動されて回転軸70の腕部材30が回転するので、
これに取り付けられた掻取部材40も回転し、これに伴
いエツジ部43が極板20の表面を摺接移動し、前記析
出沈殿物を掻取るようになり、電解処理中モータ90を
連続回転させればこの掻取操作を連続させることができ
るので、排水の電解処理作業を中断させることなく、常
に継続稼働することができる排水の電解処理装置を提供
することができる。According to the present invention, the precipitate deposited by electrolysis and deposited or attached to the electrode plate 20 is rotationally transmitted by the drive of the motor 90 and the arm member 30 of the rotating shaft 70 rotates.
The scraping member 40 attached to this also rotates, and the edge portion 43 moves in sliding contact with the surface of the electrode plate 20 to scrape off the precipitate, causing the motor 90 to continuously rotate during the electrolytic treatment. Since this scraping operation can be continued, it is possible to provide a wastewater electrolytic treatment apparatus that can be continuously operated without interrupting the wastewater electrolytic treatment work.
本発明はまた、前記排水の電解処理装置において、排水
は電解槽1内で、各極板20間とそれぞれの流通孔23
とにより形成されるジグザグ通路を回流し、その間に電
解処理されると共に、沈殿物は前記掻取操作により絶え
ず掻取られすぐに前記流出口52より排出されるので、
沈殿物が流路に停滞堆積せず、従って水流が妨害される
ことがなく、排水が強制的に所定のジグザグ通路を辿り
、よどみなくかつ十分に電解極板と接触することができ
、ほぼ完全に処理が受けられる。The present invention also provides the electrolytic treatment device for wastewater, in which the wastewater is distributed between each electrode plate 20 and through each communication hole 23 in the electrolytic cell 1.
The precipitate is circulated through the zigzag passage formed by the above, and is electrolytically treated during that time, and the precipitate is constantly scraped off by the scraping operation and immediately discharged from the outlet 52.
Precipitates do not stagnate and accumulate in the flow path, so the water flow is not obstructed, and the waste water is forced to follow a predetermined zigzag path and can fully contact the electrolytic electrode plate without stagnation, resulting in almost complete flow. can be processed.
本発明はまた、前記排水の電解処理装置において、多数
節の節部材10を上下方向へ積層状に組み合わせ、上蓋
部材50と底蓋部材60と共にタイロッド19により集
成してなる電解槽の槽本体1と、この槽本体1内部に、
それぞれ各節部材10に1枚ずつ対応して電解極板20
が保持される構成とするので、排水の容量に対応して任
意に節部材10及び極板20を加減することができ、し
たがって、排水処理容量が弾力的に増減可能な電解処理
装置を提供することができる。The present invention also provides a tank body 1 of an electrolytic cell in which a plurality of joint members 10 are vertically stacked and assembled together with a top cover member 50 and a bottom cover member 60 by a tie rod 19 in the electrolytic treatment apparatus for wastewater. And inside this tank body 1,
One electrolytic electrode plate 20 corresponds to each joint member 10.
Since the structure is such that the capacity of the wastewater is maintained, the joint members 10 and the electrode plates 20 can be arbitrarily adjusted according to the capacity of the wastewater, thus providing an electrolytic treatment apparatus in which the wastewater treatment capacity can be elastically increased or decreased. be able to.
第1図は本発明の装置の一実施例の部分破断正面図、第
2図は第1図の装置の主要部の分解斜視図、第3図(a
)、 (b)、 (C1はそれぞれ第1図中の要部を説
明するための局部拡大断面図、第4図は腕部材に取付け
られた掻取部材を示す側面図、第5図は第1図の装置の
A−A線断面図、第6図は第1図の装置の電解槽内の流
路説明のための略示線図である。
図中、1は電解槽本体、IOはフープ状節部材、20は
電解極板、23は流通孔、30は腕部材、40は掻取部
材、43は掻取部材のエツジ部、70は回転軸、90は
モータ。FIG. 1 is a partially cutaway front view of one embodiment of the device of the present invention, FIG. 2 is an exploded perspective view of the main parts of the device in FIG. 1, and FIG.
), (b), (C1 is a locally enlarged cross-sectional view for explaining the main parts in FIG. 1, FIG. 4 is a side view showing the scraping member attached to the arm member, and FIG. 1 is a sectional view taken along the line A-A of the device shown in FIG. 1, and FIG. 6 is a schematic diagram for explaining the flow path in the electrolytic cell of the device shown in FIG. 1. In the figure, 1 is the electrolytic cell main body, and IO is A hoop-shaped joint member, 20 an electrolytic electrode plate, 23 a communication hole, 30 an arm member, 40 a scraping member, 43 an edge portion of the scraping member, 70 a rotating shaft, and 90 a motor.
Claims (1)
の互いに絶縁状態の陰陽両極性の電解極板(20)を平
行に配置し、排水を前記両極板間に回流させると同時に
、両極板に電流を通すようにしてなる排水の電解処理装
置において、隣接して対向する前記陰陽両極板(20)
の間に、これらの対向両極板(20)の表面に両側縁エ
ッジ部(43)を当接して駆動手段によって移動されて
、それにより前記両極板(20)の表面を摺動する絶縁
体掻取部材(40)を設けてなることを特徴とする排水
電解処理装置。 2、前記掻取部材(40)が、弾性変形可能な樹脂によ
り当接摺動する両側縁がエッジ部(43)をなすように
形成され、そして前記駆動手段が、各極板(20)のほ
ぼ中心部を貫通するように軸架されてモータ(90)に
より駆動される回転軸(70)と、回転軸の各極板間の
位置からほぼ回転半径方向へ突設された前記掻取部材(
40)を保持する腕部材(30)とにより構成される、
請求項1記載の排水電解処理装置。 3、前記各極板(20)が、ほぼ水平面に沿って下から
上へ平行配置され、かつそれぞれの外周縁部が電解槽本
体(1)の内壁と水密に連接されると共に、各極板には
排水を流通させるための流通孔(23)が貫設されてい
て、各極板(20)はこれらの流通孔(23)が隣接極
板どうしでは互いにそれらの極板の相対する側に位置す
るように配置される、請求項2記載の排水電解処理装置
。 4、前記電解槽本体(1)が、各極板(20)ごとに1
個ずつの独自に1枚の極板を水密保持可能なフープ状節
部材(10)を相互に水密に連接させて構成される、請
求項3記載の排水電解処理装置。[Claims] 1. Inside the electrolytic cell body (1), planar electrolyte plates (20) of negative and positive polarity, which are insulated from each other, are arranged in parallel at regular intervals, and the wastewater is drained from the electrolyte plates (20). In an electrolytic treatment device for wastewater, which circulates current between the two electrode plates and at the same time passes current through the two electrode plates, the positive and negative electrode plates (20) are adjacently opposed to each other.
During this period, the insulator scraper is moved by the drive means with its side edge portions (43) in contact with the surfaces of these opposing bipolar plates (20), thereby sliding on the surfaces of the bipolar plates (20). A wastewater electrolytic treatment device characterized by being provided with a handle member (40). 2. The scraping member (40) is formed of elastically deformable resin so that both side edges that come into contact and slide form edge portions (43), and the driving means is configured to drive each electrode plate (20). A rotating shaft (70) that is mounted so as to pass through the center thereof and driven by a motor (90), and the scraping member that protrudes substantially in the direction of the rotation radius from a position between the respective electrode plates of the rotating shaft. (
and an arm member (30) holding the arm member (40).
The wastewater electrolytic treatment apparatus according to claim 1. 3. Each of the electrode plates (20) is arranged in parallel from bottom to top along a substantially horizontal plane, and each outer peripheral edge is watertightly connected to the inner wall of the electrolytic cell body (1), and each of the electrode plates A through hole (23) for distributing wastewater is provided in each plate (20). The wastewater electrolytic treatment device according to claim 2, wherein the wastewater electrolytic treatment device is arranged so as to be located in the same position. 4. The electrolytic cell body (1) has one for each electrode plate (20).
4. The wastewater electrolytic treatment apparatus according to claim 3, wherein the hoop-shaped joint members (10) each capable of holding one electrode plate watertightly are connected to each other in a watertight manner.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9417790A JPH03293091A (en) | 1990-04-11 | 1990-04-11 | Waste water electrolyzing device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9417790A JPH03293091A (en) | 1990-04-11 | 1990-04-11 | Waste water electrolyzing device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03293091A true JPH03293091A (en) | 1991-12-24 |
Family
ID=14103062
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9417790A Pending JPH03293091A (en) | 1990-04-11 | 1990-04-11 | Waste water electrolyzing device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03293091A (en) |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4934419A (en) * | 1972-07-31 | 1974-03-29 | ||
JPS5235281U (en) * | 1975-09-03 | 1977-03-12 | ||
US4123339A (en) * | 1975-02-07 | 1978-10-31 | Andco Industries, Inc. | Method and apparatus for electrochemical contaminant removal from liquid media |
JPS5579086A (en) * | 1978-12-12 | 1980-06-14 | Moru Eng Kk | Electrolytic treating method for waste water |
JPS5951066B2 (en) * | 1978-04-17 | 1984-12-12 | ソニー株式会社 | Recording/playback device |
-
1990
- 1990-04-11 JP JP9417790A patent/JPH03293091A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4934419A (en) * | 1972-07-31 | 1974-03-29 | ||
US4123339A (en) * | 1975-02-07 | 1978-10-31 | Andco Industries, Inc. | Method and apparatus for electrochemical contaminant removal from liquid media |
JPS5235281U (en) * | 1975-09-03 | 1977-03-12 | ||
JPS5951066B2 (en) * | 1978-04-17 | 1984-12-12 | ソニー株式会社 | Recording/playback device |
JPS5579086A (en) * | 1978-12-12 | 1980-06-14 | Moru Eng Kk | Electrolytic treating method for waste water |
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